Fuel cell with randomly-dispersed carbon fibers in a backing layer

1. A method of operating a fuel cell ( 40 ) for producing electricity from reducing fluid and oxygen containing oxidant reactant streams flowing through the fuel cell ( 40 ), comprising the steps of:

a. providing a first catalyst ( 12 ′) and a second catalyst ( 14 ′) secured to opposed surfaces of an electrolyte ( 16 ′);

b. defining a first flow field ( 26 ′) secured in fluid communication with the first catalyst ( 12 ′), the first flow field ( 26 ′) defining a plurality of flow channels ( 30 A′, 30 B′, 30 C′, 30 D′) between a plurality of ribs ( 32 A′, 32 B′, 32 C′, 32 D′, 32 E′) of the first flow field ( 26 ′);

c. providing a backing layer ( 42 ) secured between and in fluid communication with the first flow field ( 26 ′) and the first catalyst ( 12 ′);

d. preventing the backing layer ( 42 ) from deforming into the flow channels ( 30 A′, 30 B′, 30 C′, 30 D′) during operation of the fuel cell ( 40 ) by the backing layer ( 42 ) including;

i. between 5 wt % and 25 wt % carbon black;

ii. between 50 wt % and 90 wt % carbon fibers ( 44 ), where the carbon fibers ( 44 ) have a length that is at least twice as long as a width ( 46 ) of a widest flow channel ( 30 ′D), wherein the width ( 46 ) of the widest flow channel ( 30 ′D) is a shortest distance between flow field ribs ( 32 D′, 32 E′) defining the widest flow channel ( 30 D′) of the first flow field ( 26 ′);

iii. between 5 wt % and 25 wt % of a hydrophobic polymer; and,

iv. the carbon fibers ( 44 ) being randomly dispersed with the carbon black and hydrophobic polymer so that the resulting backing layer ( 42 ) has a thickness between the first catalyst ( 12 ′) and the first flow field ( 26 ′) of between about 25 and 250 microns, and a compressive strength greater than 5 kgf/cm 2 .

2. A method of manufacturing a fuel cell ( 40 ) comprising the steps of:

a. securing a cathode diffusion layer ( 20 ′) to a cathode substrate ( 24 ′);

b. securing an anode catalyst ( 12 ′) and a cathode catalyst ( 14 ′) to opposed surfaces of an electrolyte ( 16 ′) to form a membrane electrode assembly;

c. bonding the cathode catalyst ( 14 ′) to the cathode diffusion layer ( 20 ′); and,

d. bonding a backing layer ( 42 ) to the anode catalyst ( 12 ′), the backing layer ( 42 ) including;

i. between 5 wt % and 25 wt % carbon black;

ii. between 50 wt % and 90 wt % carbon fibers ( 44 ), where the carbon fibers ( 44 ) have a length that is at least twice as long as a width ( 46 ) of a widest flow channel ( 30 ′D), wherein the width ( 46 ) of the widest flow channel ( 30 ′D) is a shortest distance between flow field ribs ( 32 D′, 32 E′) defining the widest flow channel ( 30 D′) of the first flow field ( 26 ′)

iii. between 5 wt % and 25 wt % of a hydrophobic polymer;

iv. the carbon fibers ( 44 ) being randomly dispersed with the carbon black and hydrophobic polymer so that the resulting backing layer ( 42 ) has a thickness between the first catalyst ( 12 ′) and the first flow field ( 26 ′) of between about 25and 250 microns, and a compressive strength greater than 5 kgf/cm 2 ; and,

v. so that the backing layer ( 42 ) is prevented from deforming into the flow channels ( 30 A′, 30 B′, 30 C′, 30 D′) during operation of the fuel cell ( 40 ).